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采用吸附工艺去除工业生产废水中的有机汞硫柳汞。

Use of adsorption process to remove organic mercury thimerosal from industrial process wastewater.

作者信息

Velicu Magdalena, Fu Hongxiang, Suri Rominder P S, Woods Kevin

机构信息

Villanova Center for the Environment, Villanova University, 800 Lancaster Avenue, Villanova, PA 19085, USA.

出版信息

J Hazard Mater. 2007 Sep 30;148(3):599-605. doi: 10.1016/j.jhazmat.2007.03.015. Epub 2007 Mar 12.

DOI:10.1016/j.jhazmat.2007.03.015
PMID:17459583
Abstract

Carbon adsorption process is tested for removal of high concentration of organic mercury (thimerosal) from industrial process wastewater, in batch and continuously flow through column systems. The organic mercury concentration in the process wastewater is about 1123 mg/L due to the thimerosal compound. Four commercially available adsorbents are tested for mercury removal and they are: Calgon F-400 granular activated carbon (GAC), CB II GAC, Mersorb GAC and an ion-exchange resin Amberlite GT73. The adsorption capacity of each adsorbent is described by the Freundlich isotherm model at pH 3.0, 9.5 and 11.0 in batch isotherm experiments. Acidic pH was favorable for thimerosal adsorption onto the GACs. Columns-in-series experiments are conducted with 30-180 min empty bed contact times (EBCTs). Mercury breakthrough of 30 mg/L occurred after about 47 h (96 Bed Volume Fed (BVF)) of operation, and 97 h (197 BVF) with 120 min EBCT and 180 min EBCT, respectively. Most of the mercury removal is attributed to the 1st adsorbent column. Increase in contact time by additional adsorbent columns did not lower the effluent mercury concentration below 30 mg/L. However, at a lower influent wastewater pH 3, the mercury effluent concentration decreased to less than 7 mg/L for up to 90 h of column operation (183 BVF).

摘要

采用间歇式和连续流柱系统对碳吸附工艺去除工业生产废水中高浓度有机汞(硫柳汞)进行了测试。由于硫柳汞化合物的存在,该工艺废水中有机汞浓度约为1123mg/L。对四种市售吸附剂进行了汞去除测试,它们分别是:卡尔冈F-400颗粒活性炭(GAC)、CB II GAC、Mersorb GAC和离子交换树脂Amberlite GT73。在间歇等温实验中,通过Freundlich等温模型描述了每种吸附剂在pH值为3.0、9.5和11.0时的吸附容量。酸性pH值有利于硫柳汞吸附到GAC上。进行了串联柱实验,空床接触时间(EBCT)为30 - 180分钟。在运行约47小时(96倍床体积进料(BVF))后出现30mg/L的汞穿透,在EBCT为120分钟和180分钟时,分别在97小时(197 BVF)出现汞穿透。大部分汞的去除归因于第一个吸附柱。增加吸附柱数量并延长接触时间并没有使出水汞浓度降至30mg/L以下。然而,在较低的进水废水pH值为3时,在长达90小时的柱运行(183 BVF)期间,汞的出水浓度降至7mg/L以下。

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